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George's Service <br /> Remedial Action Work Plan <br /> Project No.425.2 <br /> June 30,2011 <br /> In addition, pump and treat may not be effective at this site for the following reasons: <br /> • The length of time a pump and treat system would require to achieve remediation, <br /> • The large volumes of groundwater needed to be extracted for a pump and treat system <br /> to be effective to extract dissolved-phase hydrocarbons and/or achieve hydraulic <br /> control to prevent offsite migration <br /> • No capability for Source Area removal within the unsaturated zone, <br /> • The possibility of renewed groundwater impact subsequent to system shutdown, and, <br /> • The likelihood that treated discharge from a pomp and treat system would be flow- <br /> restricted by disposal options. <br /> 5.3. In Situ Chemical Oxidization <br /> The process of in slat chemical oxidation has been used successfully in many applications. <br /> Advanced Oxidation Processes (AOPs) are processes that create and use a highly reactive <br /> radical that effectively oxidizes organic compounds by chemical reaction. The most <br /> prominently used radical is the hydroxyl radical, designated as OH. The OH ion will <br /> capture a hydrogen atom from a molecule of contaminant, which then causes the contaminant <br /> molecule to become unstable and breakdown. <br /> The AOPs have been very successful at treating gasoline compounds and the gasoline <br /> oxygenated fuel compounds. AOPs are promising because they quickly destroy the <br /> contaminant rather than just augmenting the relatively slow biological processes at the site. <br /> It is noted that a byproduct of injecting oxidizing agents is an increase in the oxygen content <br /> of the subsurface to promote biodegradation rates. <br /> The basic chemistry of reduction-oxidation (Redox) reactions is a combination of chemical <br /> reactions (changes in chemical bonding) and the transfer of electrons. A more detailed <br /> explanation is: specific bonds are broken while others are formed when a donor gives up an <br /> electron (e) and a receptor acquires the e-. In the case of petroleum contamination, BTEX <br /> and TPH-G are reduced (gain of electrons and a decrease in valence) and in an aerobic <br /> environment oxygen is oxidized (loss of electrons and increase in valence). In an anaerobic <br /> environment, oxygen has been depleted by this reaction and mineral compounds, such as <br /> Mn02, NO3, Fe(0)3, SO4 and H+, become the a donor(listed in decreasing Eh values). <br /> The half-life of ozone in the presence of water is typically 30 minutes at standard <br /> temperatures and pressures, but it can be longer in subsurface environments. Depending on <br /> the concentrations of contaminants present in the subsurface, delivery may need to be <br /> sustained over a longer period of time than the other oxidants. The contaminants are treated <br /> in situ, converted to innocuous and/or natural occurring compounds [e.g. H2O, CO2, and 02 <br /> halide ions]. Because ozone is a gas, it can easily be used to remediate vadose zone <br /> contamination. As a side benefit, ozone provides oxygen to the microbial community, as it <br /> decomposes, which can aid in bioremediation. <br /> otological Technics/a. 9 <br /> 4252 RAP.docx <br />